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US9522386B2ActiveUtilityPatentIndex 40

Catalyst and a process for catalytic conversion of carbon dioxide-containing gas and hydrogen streams to hydrocarbons

Assignee: B G NEGEV TECH AND APPLICATIONS LTD AT BEN-GURION UNIVPriority: Jan 17, 2013Filed: Jul 16, 2015Granted: Dec 20, 2016
Est. expiryJan 17, 2033(~6.5 yrs left)· nominal 20-yr term from priority
Inventors:LANDAU MIRONHERSKOWITZ MORDECHAIVIDRUK ROKSANA
B01J 2235/00B01J 2235/30B01J 35/393B01J 23/745B01J 37/03C10G 2/332C10G 2/50B01J 37/18B01J 35/1038B01J 35/006B01J 2523/00B01J 2523/13B01J 37/08B01J 35/1014B01J 23/005B01J 37/0201B01J 27/22B01J 35/1019B01J 37/0009B01J 2523/31B01J 23/78B01J 35/1061B01J 2523/17B01J 2523/842B01J 2235/15B01J 35/613B01J 35/615B01J 35/633B01J 35/647B01J 37/009B01J 37/0236B01J 37/031B01J 37/04B01J 37/082
40
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Cited by
31
References
4
Claims

Abstract

The invention relates to a catalyst suitable for use in the hydrogenation of carbon dioxide-containing gas, said catalyst comprising spinel phase of the formula [Fe 2+ (Fe 3+ y Al 3+ 1-y ) 2 O 4 ]. Processes for preparing the catalyst and processes for the hydrogenation of carbon dioxide-containing gas in the presence of the catalyst are also disclosed.

Claims

exact text as granted — not AI-modified
The invention claimed is: 
     
       1. A catalyst suitable for use in the hydrogenation of carbon dioxide-containing gas, said catalyst comprising spinel phase of the following formula:
   [Fe 2+ (Fe 3+   y Al 3+   1-y ) 2 O 4 ]  Formula 1
 
 wherein y is from 0.25 to 0.75, having surface area of not less than 80 m 2 /gram, and wherein the catalyst is copper-free and is devoid of hematite phase, metallic iron, Fe 3 O 4  and Fe-carbide, wherein the catalyst further comprises potassium on its surface. 
 
     
     
       2. A catalyst according to  claim 1 , wherein y is from 0.3 to 0.7. 
     
     
       3. A catalyst according to  claim 1 , wherein the spinel of Formula 1 has average crystal size in the range from 1.5 to 3 nm, as measured by X-Ray diffraction (XRD). 
     
     
       4. A catalyst according to  claim 1 , having surface area between 80 m 2 /g and 180 m 2 /g.

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